- São Paulo/SP Eficiência Energética na Indústria de Cimento Mauricio Henriques Jr. Instituto Nacional de Tecnologia (INT) Realização
Sumário Introdução Evolução do uso de energia e do consumo específico no setor Comparação internacional Tecnologias de uso eficiente de energia (Best Available Tecnologies) e discussão de alguns cases Compilação das tecnologias aplicáveis no parque brasileiro, e comentário finais
Evolução do uso de energia e do consumo específico no setor
Energy share in cement production Source: EPE, 2015.
Energy Share in Cement Production - 2014 Petroleum Coke 70,4% Others 11,9% Electricity 12,9% Mineral Coal 2,3% Fuel Oil 0,3% Charcoal 2,3% Source: EPE, 2015.
Fuel share in Cement Production - 2013 2013 Conventional Fossil Fuels 82,5% Coal + anthracite + waste coal 1,5% Petcoke 80,5% (ultra) Heavy fuel 0,2% Diesel oil 0,2% Biomass Fuels 9,6% Dried sewage sludge 0,0% wood, non impregnated saw dust 0,1% Agricultural, organic, charcoal 4,7% Other biomass 4,8% Fossil Waste 7,9% Waste oil 0,3% Tyres 4,6% Plastics 0,1% Impregnated saw dust 0,3% Mixed industrial waste 1,6% Other fossil based wastes 0,9% Source: CSI
Energy specific consumption Production 20 a 22 de Junho de 2016 Specific thermal energy consumption (GJ/t cement) 6,00 5,00 4,00 3,00 2,00 1,00 80.000 70.000 60.000 50.000 40.000 30.000 20.000 10.000 0,00 0 1960 1970 1980 1990 2000 2010 2020 Consumo térmico/produção (GJ/t) Produção (10^3 t) Source: EPE, 2015.
Specific termal consumption 20 a 22 de Junho de 2016
Thermal energy intensity cement industry in Brazil Fonte: CSI (2014)
Electricity intensity cement industry Fonte: CSI (2014)
CO2 Emissions CSI (77% of total Prod.) Source: CSI (2014)
CO2 emissions reductions possibilities
CO2 emissions reductions possibilities
CO2 emissions electricity in Brazil Emission factor of the Brazilian energy grid Source: MCTI 2016
Cement Production Process Flow Schematic and Typical Energy Efficiency Measures Source: Industrial Energy Technology Database, Institute for Industrial Productivity, http://ietd.iipnetwork.org/content/cement
Specific Thermal Energy Consumption by Rotary Kiln Type Kiln Type Heat Input, MJ/ton of clinker Wet 5,860 6,280 Long Dry (LD) 4,600 1 Stage Cyclone Preheater (SP) 4,180 2 Stage Cyclone Preheater (SP) 3,770 4 Stage Cyclone Preheater (SP) 3,550 4 Stage Cyclone Preheater plus Calciner (PC) 3,140 5 Stage Cyclone Preheater plus Calciner (PC) plus high efficiency cooler 6 Stage Cyclone Preheater plus Calciner (PC) plus high efficiency cooler 3,010 <2,930 Source: Based on Madlool 2011
Energy saving measures and technologies (selected) 1- High efficiency fan and VSD for mill vent 2- Pre-grinding to ball mills 3- Variable speed drive & high efficiency fan 4- Process controls and optimization 5- Waste Heat Recovery for power production 6- Low pressure drop cyclones for suspension preheater 7- Improved burnability using mineralizers 8- Optimizing heat recovery 9- VSD for cooler fan 10- Process control and management in finish grinding 11- Replacing ball mill with vertical roller mill, HPGR or Horizontal mill 12- Optimizing the operation of a cement mill 13- High pressure roller press as a pregrinding to ball mill 14- High-efficiency classifiers
Summary energy and CO2 reductions 20 a 22 de Junho de 2016 En. Eff. Measures Electricity Reduction Unit Thermal reduction Unit GHG Reduction Unit High efficiency fan and VSD for mill vent 0,36 kwh/t-clinker - 0,04 kgco2/t-clinker Pre-grinding to ball mills 0,8 kwh/t-raw mat. - 0,10 kgco2/t-raw mat. Variable speed drive & high efficiency fan 0,16 kwh/t-clinker - 0,02 kgco2/t-clinker Process controls and optimization - 0,111 GJ/t-clinker 9,22 kgco2/t-clinker Waste Heat Recovery for power production 25 kwh/t-clinker - 3,12 kgco2/t-clinker Low pressure drop cyclones for suspension preheater 0,13 kwh/t-clinker - 0,02 kgco2/t-clinker Improved burnability using mineralizers - 0,115 GJ/t clinker 9,55 kgco2/t-clinker Optimizing heat recovery - 0,065 GJ/t clinker 5,40 kgco2/t-clinker VSD for cooler fan 0,10 kwh/t clinker - 0,01 kgco2/t-clinker Process control and management in finish grinding 3,5 kwh/t cement - 0,44 kgco2/t-cem. Replacing a ball mill with vertical roller mill, HPGR or horiz.mill in finish grinding 9 kwh/t cement - 1,12 kgco2/t-cem. Optimizing the operation of a cement mill 2 kwh/t cement - 0,25 kgco2/t-cem. High pressure roller press as a pregrinding to ball mill 10 kwh/t cement - 1,25 kgco2/t-cem. High-efficiency classifiers 5 kwh/t cement - 0,62 kgco2/t-cem.
Process controls and optimization - Clinker Making (On-line) Monitoring & analyses of physical & chemical characteristics Automated weighing & blending control Combustion management fuel grinding, air & mass flow, exhaust gas management, burner management, cooler operation Expert control (fuzzy-logic, rule-based-control) and modelpredictive systems. Potential Benefits - Improved product quality; improved heat recovery; lower refractory consumption; reduced maintenance; higher productivity
Process controls and optimization - Clinker Making Schematic depiction of control points and parameters in a kiln system control and management system. Source: FLSmidth
Process controls and optimization - Clinker Making Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016). Estimated energy saving in Brazil: ~ 3% Tech. penetration in BR 2014: 38% 2030: 66% 2050: 99%
Waste Heat Recovery for power production- Clinker Making
Waste Heat Recovery for power 20 a 22 de Junho de 2016 Tech. penetration in BR 2014: 0% 2030: 33% 2050: 33% Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
Improved burnability using mineralizers Clinker Making Mineralizadores (fluoretos) são substâncias que promovem a formação de compostos de clinquer sem participar nas reacções de formação. São particularmente eficazes e promovem a formação de silicato tricálcico. Possibilitam uma menor demanda de energia uma vez que reduzem a temperatura na sinterização do clínquer. O potencial desta tecnologia é limitado. Enquanto a adição de mineralizadores em quantidades menores pode melhorar a qualidade do produto, quantidades maiores podem ter impactos adversos na qualidade do produto e na operação do forno devido à formação de revestimentos. Main Influencing Parameters Chemical properties of the raw mix and mineralizers Mineralogy of its component materials and its fineness Raw mix control and kiln feed homogenization CO2 intensity of fuel mix Conditions, Barriers and Constraints Costs of mineralizers Grindability of clinker can deteriorate Increased coating formation in the sintering zone Impact on clinker quality Impact on kiln operation and product properties Health problems given fluor emission of the kiln Tech. penetration in BR 2014: 5% 2030: 5% 2050: 5%
Optimizing heat recovery- Clinker Making Clinker cooler optimization aims to maximize heat recovery, minimize clinker temperature and reduce specific fuel consumption. This may also improve product quality and emission levels. Heat recovery can be improved through reduction of excess air volume, control of clinker bed depth and new grates such as ring grates. A recent innovation in clinker coolers is the installation of a static grate section at the hot end of the clinker cooler. Additional heat recovery results in reduced energy use in the kiln and precalciner, due to higher combustion air temperatures. Fixed static inlet section for a clinker cooler Source: Institute for Industrial Productivity (IIP) & ECONOLER (2016).
Optimizing heat recovery- Clinker Making Energy Performance 0.05 to 0.08 GJ/t-clinker savings are reported through the improved operation of the grate cooler, and savings of 0.16 GJ/t-clinker are reported for retrofitting a grate cooler. Fixed static inlet section for a clinker coolered by an increase in electricity use of 2.0 kwh/t clinker. Installation of a static grate section could improve the heat recovery rates by 2 to 5 percent. Tech. penetration in BR 2014: 64% 2030: 99% 2050: 99%
Replacing a ball mill with vertical roller mill, HPGR or horizontal mill in finish grinding Vertical Roller Mills (VRM), High-Pressure Roller Press (HPGR) and Horizontal Mills offer more efficient grinding High Pressure Roller Press in finish grinding. FLSmidth, 2010 Basic layout of cement grinding using horizontal mill. Fives Fcb Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
Replacing ball mill with more efficient technologies Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
Replacing ball mill with more efficient technologies In Brazil - power savings are estimated in 9 kwh/ton cement using roller mill Costs (Brazil): US$ 70/t cement capacity Tech. penetration in BR 2014: 13% 2030: 13% 2050: 13% Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
High pressure roller press for pre-grinding (as a coarse grinding prior to fine grinding in a ball mill) Efficiency of ball mills is low, and there is limited opportunity to improve both coarse and fine grinding performance by ball selection Install vertical mill for coarse grinding before ball mill existing ball mill used exclusively for fine grinding Potential for productivity increase between 50 100 percent Implementation Factors: More applicable to plants where the total replacement of ball-mills is not feasible and capacity increases are desirable High pressure roller press as a pre-grinding to ball mill (FLSmidth, 2010) High pressure roller press as a semi-finish pre-grinder with two stage separator (FLSmidth, 2010)
High pressure roller press for pre-grinding Tech. penetration in BR 2014: 0% 2030: 0% 2050: 0%
High-efficiency classifiers Finish Grinding Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
High-efficiency classifiers Finish Grinding Tech. penetration in BR 2014: 70% 2030: 80% 2050: 80% Source: Institute for Industrial Productivity (IIP) and ECONOLER (2016).
General energy savings measures (house keeping) High efficiency motors Use of variable speed drives (VSD): Mill vent raw material Fuel Preparation Preheaters Cooler fans Cement mill vent Preventative maintenance Compressed air system maintenance and optimization Reducing leaks in comp air system Compressor controls Energy Savings: 1% or 2% of the electricity consumption of the cement plant Tech. penetration in BR 2014: 13% 2030: 33% 2050: 66%
Summary energy and CO2 reductions Energy Efficient Measures Electricity Reduction Thermal Reduction GHG Reduction Pre-grinding to ball mills 0.8 kwh/t-raw mat. - 0.10 kgco2/t-raw mat. Process controls and optimization - 0.111 GJ/t-clinker 9.22 kgco2/t-clinker Waste Heat Recovery for power production 25 kwh/t-clinker - 3.12 kgco2/t-clinker Low pressure drop cyclones for suspension preheater 0.135 kwh/t-clinker - 0.02 kgco2/t-clinker Improved burnability using mineralizers - 0.115 GJ/t clinker 9.55 kgco2/t-clinker Optimizing heat recovery - 0.065 GJ/t clinker 5.40 kgco2/t-clinker Process control and management in finish grinding 3.5 kwh/t cement - 0.44 kgco2/t-cement Replacing a ball mill with vertical roller mill, HPGR or Horizontal mill in finish grinding 9 kwh/t cement - 1.12 kgco2/t-cement Optimizing operation of a cement mill 2 kwh/t cement - 0.25 kgco2/t-cement High pressure roller press as a pregrinding to ball mill 10 kwh/t cement - 1.25 kgco2/t-cement High-efficiency classifiers 5 kwh/t cement - 0.62 kgco2/t-cement General E.Ef. measures 1 kwh/t cement - 0.12 kgco2/t-cement Source: IIP & ECONOLER (2016) and INT.
Summary table - costs and technology penetration En. Eff. Measures Costs (Brazil) Penetration (%) 2014 Penetration (%) 2030 Penetration (%) 2050 Pre-grinding to ball mills US$ 18,6 million 2% 2% 2% Process controls and optimization US$ 0,6 a 1,7 t/clinker 38% 66% 99% Waste Heat Recovery for power production US$ 3.000/kWe 0% 33% 33% Low pressure drop cyclones for suspension preheater US$ 26,8 million 60% 60% 60% Improved burnability using mineralizers US$ 0,6 a 3 t/clinker 5% 3% 3% Optimizing heat recovery US$ 0,47 t/clinker 64% 99% 99% Process control and management in finish grinding US$ 1,2 t/clinker 61% 66% 66% Replacing ball mill with vertical roller mill, HPGR or horizontal mill US$ 70 t/cement-cap 13% 13% 13% Optimizing the operation of a cement mill US$ 0,39 t/cement 33% 50% 66% High pressure roller press as a pregrinding to ball mill US$ 30 million 0% 0% 0% High-efficiency classifiers US$ 4 t/year 70% 80% 80% General measures 0,30 US$/t-cement 13% 33% 66% Source: IIP & ECONOLER (2016) and INT.
Muito Obrigado Mauricio F. Henriques Jr. Instituto Nacional de Tecnologia INT mauricio.henriques@int.gov.br 21 2123.1256